Functionalized polyolefin capillaries for open tubular ion chromatography

ABSTRACT

Open tubular capillary columns for liquid and ion chromatography, based upon an ionically impermeable polyolefin capillary having a bore with a sulfonate-group- or amine-group-functionalized internal surface. The capillary columns may include a coating of ion exchanging nanoparticles electrostatically bound to the functionalized internal surface. The capillary columns may be made by exposing the interior surface to a sulfonating reagent comprising chlorosulfonic acid (ClSO 3 H), preferably from 85 wt % to 95 wt % chlorosulfonic acid at a process temperature of 20 to 25° C. The interior surface may be subsequently exposed to an asymmetrical diamine to form a sulfonic mid-linkage to the diamine, i.e., to form a sulfonamide-linked, amine-group-functionalized internal surface. The coating may be provided by subsequently exposing the interior surface to an aqueous suspension of ion exchanging nanoparticles to electrostatically bond the ion exchanging nanoparticles to the functionalized internal surface.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a divisional of U.S. patent application Ser. No.15/395,202 filed on Dec. 30, 2016, which claims the benefit of U.S.Provisional Patent Application No. 62/402,354 filed on Sep. 30, 2016,both of which are incorporated herein by reference in their entirety.

GOVERNMENT SUPPORT

This invention was made with government support under Grant No.NNX11AO76G awarded by NASA. The government has certain rights in theinvention.

BACKGROUND

In chromatography systems, separation columns are arguably the mostimportant functional element of the system. Of the various monolithic,packed, and open tubular (OT) column options used in liquid/ionchromatography, the latter type require the least pressure, permittingthe use of simple and easily miniaturizable pneumatic pumpingcomponents. A recent review specifically addresses preparation andapplication trends in open tubular (OT) capillary columns in theseparation sciences [1], however most of the reported work pertains tothe use of fused silica capillaries, which are not compatible withextremes of pH. In particular, anion exchanger (AEX) coated silicacapillaries have previously been used in the single column mode withmodestly alkaline or neutral pH eluents [2], however the electrostaticattachment of such materials to surface silanol (—SiOH) functionalgroups is not stable over long periods of time in significantconcentrations of strong base (e.g., 50 mM NaOH), so that work withAEX-functionalized silica capillaries has generally been limited toapplications not requiring extremes of pH [3, 4]. Whilepolymethylmethacrylate (PMMA) capillaries are known to be substantiallymore stable in strong base than silica [5, 6], and have surfacecarboxylate (—COOH) functional groups that can electrostatically bindAEX materials more strongly than the weaker silanol groups of fusedsilica capillaries, the applicants have found that AEX latex attachmentto PMMA is gradually lost in ˜>5 millimolar (mM) hydroxide over longperiods of time. Furthermore, neither of the above materials permit theattachment of cation exchanger (CEX) latex particles to the surface ofsuch capillaries, since a positive surface charge is required forattachment of CEX latex to the capillary surface and neither fusedsilica nor PMMA capillaries provide a pH-stable platform for modifyingthe capillary surface so as to introduce positive surface charges.Consequently, these substrates are not suitable for use in isocratic orgradient suppressed ion chromatography applications.

SUMMARY

Novel polyolefin based open tubular capillary ion exchange columns aredisclosed, preferably having internal diameters of 5 to 50 μm or, evenmore preferably, 10 to 30 μm. In some implementations, the polyolefinbased capillaries have a partially sulfonate-group-functionalizedinternal surface. In other implementations, the polyolefin basedcapillaries have a sulfonic mid-linkage to a diamine-group, i.e., asulfonamide-linked, amine-group-functionalized internal surface. Thosefunctionalized internal surfaces may be manufactured by exposing theinterior of a polyolefin capillary to a sulfonating reagent comprisingchlorosulfonic acid (ClSO₃H; 85-95% w/w) and a diluent such as glacialacetic acid (CH₃COOH), anhydrous sulfuric acid (H₂SO₄), or a combinationthereof (balance) for a period of 2 to 10 hours at room temperature(20-25° C.), and then either converting the resultant chlorosulfonicmoieties to sulfonic acid moieties via hydrolysis or linking theresultant chlorosulfonic moieties to an asymmetrical diamine compound(optionally with further modification of the linked compound to form aquaternary amine moiety). The cation ion exchange capacity of theresultant capillary column is controlled by the chlorosulfonic acidconcentration and sulfonation time, and may be as high as 300 peq/mm².

In some implementations, the functionalized internal surface of thecapillary column is coated with a layer of ion exchanging nanoparticles.A coated surface may be manufactured by exposing asulfonate-group-functionalized internal surface to, for example, anaqueous suspension of quaternary-ammonium-group-functionalized latexnanoparticles, whereupon electrostatic attraction between the sulfonateand anion exchanging functional groups electrostatically bonds thenanoparticles to the internal surface. The anion exchange capacity ofthe resultant column may be as high as 20 peq/mm². A coated surface mayalso be manufactured by exposing a sulfonamide-linked,amine-group-functionalized internal surface to, for example, an aqueoussuspension of sulfonate-group- or carboxylate-group-functionalized latexnanoparticles, producing similar electrostatic bonding of thenanoparticles to the internal surface.

In some implementations, the polyolefin based capillary is formed as ahelical coil having a bend radius of between 0.4 mm and 2.0 mm. Thehelical coil shape may be manufactured by immersing some or all of acapillary in a heated fluid and then wrapping a section of the capillaryaround a form.

The applicants have found that the bonding of anion exchangingnanoparticles is much stronger to sulfonated COP (—SO₃H functionalgroups) than to hydroxylated silica (—OH functional groups) orpolymethylmethacrylate (—COOH functional groups). Using exemplarynanoparticles based on AEX-functionalized latex, the applicants showsufficiently persistent bonding to enable use in ion exchangechromatography systems with practical hydroxide eluent concentrationsover long periods of time, paving the way for many SuppressedConductometric Capillary Ion Chromatography (SCCIC) applications. Theapplicants have also determined that when the interior surface isheavily sulfonated, neutral analytes may elute after anion analytes inboth coated and uncoated columns due to anion exclusion effects onanionic analytes. The degree of sulfonation of the internal surface maybe thus be varied to alter the position of the water dip, to cause aseparation between elemental anions, organic anions, and neutrals (suchas alcohols), and/or to cause a separation among aprotic neutrals.Similarly, the degree of sulfonation, upon reaction with a suitableasymmetrical diamine, can allow for the manipulation of the timing ofthe water dip to beneficially position the dip's effect upon detectorresponse to a time that will not interfere with the detection of earlyeluting alkali metal cations or weakly retained amines. Finally, theapplicants have found that these columns, if softened at modestlyelevated temperatures (e.g., in boiling water), can be coiled down to <1mm coil radii, producing very low-volume, low-dispersion separationcolumns due to the beneficial effects of centrifugal force on masstransfer to the stationary phase (the sulfonated polyolefin materialand, when present, the electrostatically bound AEX nanoparticlecoating).

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic cross-sectional view of an exemplary open tubularcapillary ion exchange column.

FIG. 2 is a flow chart of a process for manufacturing a polyolefin basedopen tubular capillary ion exchange column without (through step 240)and with (through step 260) a coating of AEX nanoparticles.

FIG. 3 is a schematic diagram of an exemplary system for sulfonatingpolyolefin capillaries.

FIG. 4 is a flow chart of a process for manufacturing a polyolefin basedopen tubular capillary ion exchange column without (through step 440 or450) and with (through step 460) a coating of CEX nanoparticles.

FIG. 5 is a plot illustrating the extent of sulfonation (as measured bycation exchange capacity) versus time of exposure to a sulfonatingreagent.

FIG. 6 shows a cation exchange capacity determination for an exemplaryopen tubular capillary ion exchange column, showing breakthrough of apumped NaOH solution at ˜18 minutes.

FIG. 7 shows chromatograms obtained by employing a heavily sulfonatedCOP based capillary column to separate (a) water and ethanol, and aheavily sulfonated, AEX latex coated COP based capillary to separate (b)early eluting inorganic anions from the sample water dip. (c) shows aseparation where a more strongly retained inorganic anion co-elutes withthe sample water dip.

FIG. 8 includes plots of baseline conductance and baseline noise (insetplot) versus time in a rinsing step 240.

FIG. 9 is a plot comparing cation exchange capacity (sulfonated COPmaterial) to anion exchange capacity (AS18 latex nanoparticle coating)for capillaries manufactured according to process 200 with varyingextents of exposure to a sulfonation reagent (90 wt % ClSO₃H: 10 wt %CH₃COOH).

FIG. 10 is a plot comparing the reproducibility of cation exchangecapacity (sulfonated COP material) and anion exchange capacity (AS18latex nanoparticle coating) in capillaries manufactured according toprocess 200.

FIGS. 11A and 11B show chromatograms for AS18 latex coated COP basedopen tubular capillary columns with 20 cm and 30 cm effective lengths,respectively, using different eluents and eluent flow rates.

FIG. 12 shows chromatograms for AS18 latex coated COP based open tubularcapillary columns using a divalent ion-based eluent at differentconcentrations and pHs.

FIG. 13 is a photograph of COP based open tubular capillary columnsafter formation into helical coils by winding ˜360 μm capillaries upon1/16 inch (1.6 mm; top) and 1/32 inch (0.8 mm; bottom) diameter rods.

FIG. 14 is a photographic end view of the bottom helically coiled columnof FIG. 13.

FIG. 15 is a fitted Van Deemter plot of chloride ion plate height versusflow velocity in straight (diamond) and helically coiled (circle) AS18latex coated COP based capillary column configurations.

FIG. 16 is a plot of applied pressure versus eluent flow velocity for anopen tubular capillary column configured as a completely straight column(733 mm effective length; circles), as a partially helically coiledcolumn (225 mm of length coiled to d_(c)=1.97 mm; diamonds), as apartially helically coiled column (455 mm of length coiled to d_(c)=1.97mm; triangles), and an almost completely helically coiled column (675 mmof length coiled to d_(c)=1.97 mm; X-s). The inset graph illustrates theexperimentally observed fit of a model of additional pressure loss, dueto coiling, versus flow velocity as described by Equation (1).

DETAILED DESCRIPTION

In describing different aspects of the polyolefin based open tubularcapillary ion exchange columns, reference is made to FIG. 1. However, itwill be appreciated that the interior regions of the illustration havebeen exaggerated and are not shown to scale. Additionally, exemplarysystems for manufacturing and using the disclosed columns are shown, butit will be appreciated that other systems may be used to carry out thedescribed manufacturing processes, and that the disclosed columns may beused in various Suppressed Conductometric Capillary Ion Chromatography(SCCIC) systems.

In general, each open tubular capillary ion exchange column 100comprises a capillary drawn from a stock of polyolefin material. In someimplementations, the material is a cycloolefin material, such as anorbornene-type (ring-opening-metathesis-polymerized8,9,10-trinorborn-2-ene) material [7, 8]. In other implementations, thematerial is a cycloolefin copolymer material, such as anorbornene-ethylene-type (chain copolymerization of8,9,10-trinorborn-2-ene with ethylene) material [7, 8]. One suchmaterial, marketed as ZEONEX® 330R by Zeon Corp. (Tokyo, Japan),exhibits a very low glass transition temperature (123° C.) [9] with theadded benefit of very low fluorescence, optical transparency down to 290nm at capillary scale thicknesses, and a small additional window ofoptical transparency centered at ˜250 nm. Capillaries may bemanufactured from cylinders (e.g., 7.35 cm in diameter×20 cm long)machined with a concentric hole (e.g., 3.97 mm or 5/32 in. i.d.) into apreform that has the same o.d./i.d. aspect ratio as the target o.d./i.d.of the capillary (e.g., 370 μm o.d. and 20 μm i.d.). Such a preform maythen be extruded into open tubular capillaries using known techniques orby a commercial extruder such as Paradigm Optics, Inc. (Vancouver,Wash., USA). Using a commercial extrusion service, applicants haveobtained capillaries having a 360 to 375 μm o.d., a 19 to 28 μm i.d.,and a bore uniformity of ±2 μm per meter. While it is well known thatcolumn efficiency and speed of separation increase with decreasingcapillary column bore diameter (with an optimum inner diameter of 0.26μm suggested theoretically for OT liquid chromatography [10]), it willbe appreciated that difficulties in column preparation, reproduciblesample injection, and detection sensitivity, as well as the potentialfor column blockage, also increase with decreasing capillary borediameter so that, in the applicants' experience, column diameters of 10to 30 μm currently provide an optimum range of compromise.

The internal surface 110 of the capillary is chemically modified tosubstitute some polymer chain hydrogen atoms with sulfonate functionalgroups, i.e., to have a sulfonate-functionalized internal surface region120 surrounded by non-functionalized and ionically impermeable material.In principle, the polyolefin material should consist of chains ofsaturated aliphatic hydrocarbon backbone and/or rings (from linear,branched, or cyclic olefin monomers); however, significant opticalabsorption below 300 nm suggests that residual olefinic moieties will bepresent in commercially available materials, and it is those moietiesthat will likely be attacked first with the formation of some α-chloroβ-alkanesulfonic acids [11]. Chlorosulfonic acid attack on the materialwill otherwise replace an H atom (reactivity: tertiary>secondary>primaryH) with a sulfonate (—SO₃H) group, liberating HCl [12]. Thus it shouldbe appreciated that sulfonation should principally, but will notexclusively, sulfonate originally unsaturated moieties.

FIG. 2 shows a process for manufacturing the sulfonate-functionalizedinternal surface 110, i.e., region 120, using chlorosulfonic acid(ClSO₃). It is important to note that this acid is an extremelyaggressive reagent that reacts explosively with water, generating H2SO4and HCl fumes and potentially causing severe burns. Thus the processpreferably includes an initial step (process step 210) of drying theinternal surface 110 of a COP capillary. For example, dry nitrogen gasmay be passed through the capillary at 60-100 psi for 5-10 min to dry itthoroughly. With a dry capillary, the process (process step 220) exposesthe internal surface 110 of the capillary to chlorosulfonic acid tosulfonate the polyolefin material. The acid may be provided as purechlorosulfonic acid, but is preferably provided in a sulfonating reagentcomprising from 85 wt % to 95 wt % chlorosulfonic acid and a balance ofa nonaqueous, chlorosulfonic acid compatible diluent. For example,glacial acetic acid (CH₃COOH), anhydrous sulfuric acid (H₂SO₄), or acombination thereof may be used as the diluent. In an exemplary system300 for performing the process, shown in FIG. 3, one end of thecapillary 302 is connected to a pressurizable reservoir 310 that isconnected to a source of dry nitrogen gas 320. The capillary may then bedried (process step 210) by simply pressurizing the reservoir 310. Afterdrying, the end of the capillary 302 may be lowered into a reagent vial330 positioned within the reservoir 310 and containing a small volume (1mL) of sulfonation reagent 332. The reagent vial 330 is preferablycovered with an inert membrane 334 to provide a measure of spillresistance, so that the end of the capillary must puncture the membraneas it is lowered to the bottom of the vial. Depending upon the lengthand bore of the capillary, the reservoir may be pressurized to 10-60 psito pump the sulfonating agent through the capillary. The other end ofthe capillary 304 may be inserted into a waste vial 340 to collectexpelled reagent for disposal. The waste vial 340 may contain anonaqueous, chlorosulfonic acid compatible diluent 342, such as glacialacetic acid, to reduce the potential effects of an inadvertent exposureto water. The waste vial may also be covered with an inert membrane 344to provide a measure of spill resistance. After exposure, the processpreferably exposes the sulfonated internal surface 110 of the capillaryto a nonaqueous, chlorosulfonic acid compatible flushing agent (processstep 230). The flushing agent used in process step 230 may be the sameas or different than the diluents mentioned above. For example, thecapillary may be pneumatically flushed by substituting a vial 350 ofglacial acetic acid for the reagent vial 330 and pressurizing thereservoir 310 to 80 psi for 30 min to remove residual chlorosulfonicacid from the capillary bore and sulfonated region 120. Alternately, thecapillary may be pneumatically flushed with a gas and any residualsulfonating agent allowed to expend itself. Then, in process step 240the chlorosulfonated internal surface 110 of the capillary may be rinsedwith deionized water or a base to hydrolyze the resultantchlorosulfonate moieties to sulfonate functional groups. For example,the column 100 may be connected to a HPLC pump and rinsed with deionizedwater at 1 to 10 μL/min for 20 to 100 hours to facilitate hydrolysis aswell as to remove residual sulfonating agent, flushing agent, or otherions and unbound chemical species, as discussed in further detail below.Alternately, the column 100 may be rinsed with a solution of at least 10mM alkali metal hydroxide for 5 to 25 hours to accelerate the rate ofhydrolysis of the chlorosulfonate moiety.

In some implementations, the sulfonate-functionalized internal surface110 of the column 100 is coated with a layer of anion exchangingnanoparticles 130. Carrying out multi-step chemistry in small borecapillaries to provide differing or mixed separation domains can bedifficult and result in low yields, while coating with functionalizednanoparticles can be accomplished by passing a suspension through anoppositely charged capillary. For the present columns, electrostaticattraction between the negatively charged sulfonate functional groups ofthe internal surface 110 and the positively charged anion exchangingfunctional groups on the exterior surface of AEX nanoparticles 130electrostatically bonds the nanoparticles to the internal surface 110,forming a monolayer that permits efficient stationary phase masstransfer to the AEX functional groups and consistent mass transferbehavior for neutrals through the nanoparticulate layer to thesulfonate-functionalized region 120. For example, the applicants haveelectrostatically bonded quaternary-ammonium-group-functionalized latexnanoparticles with a median diameter of 65 nm, manufactured by ThermoFisher Scientific (Waltham, Mass., USA) for use in its Dionex IonPacAS18 hydroxide-selective anion exchange column, to such functionalizedinternal surfaces. Referring again to FIG. 2, in process step 250 thesulfonated internal surface 110 of the capillary may be exposed to anaqueous suspension of anion exchanging nanoparticles 130. For example, asuspension of AS18 latex nanoparticles may be prepared by diluting aconcentrated suspension with neutral or modestly alkaline water (e.g., a10 mM LiOH solution) to a 10% (wt/v) suspension of nanoparticles. Itwill be appreciated that process step 250 may be performed without firstperforming process step 240, so that the suspension solution itselffacilitates hydrolysis of chlorosulfonate moieties into sulfonatefunctional groups. The suspension may be pumped through the capillaryusing the system 300, although applicants found it preferable toconserve the suspension by using two such systems, placing the other endof the capillary 304 in a vial in a second pressurizable reservoir (notshown) and alternately pressurizing one reservoir 310 while venting theother to cause the suspension to flow through the capillary, back andforth between vials. Finally, in process step 260 the coated internalsurface 110 of the capillary may be rinsed with deionized water to cleanthe coated column. For example, the column 100 may be connected to aHPLC pump and rinsed at 1 to 10 μL/min for 0.5 h to 2 h to remove thesuspension fluid and unbound residual nanoparticles from the bore.

FIG. 4 shows a related process for manufacturing a sulfonamide-linked,amine-group-functionalized internal surface 110 using chlorosulfonicacid (ClSO₃). Process steps 410-430 are identical to process steps210-230 as described above. Then, the process (process step 440) exposesthe internal surface 110 of the capillary to an asymmetrical diamine toproduce a sulfonamide-linked amine moiety. For example, the process step440 may expose the internal surface to an aminating reagent comprisingN—N-dimethylethylenediamine to produce a sulfonamide-linkeddimethylaminoalkane. It should be noted that both methyl groups in thisexemplary compound are attached to the same amine group to create theasymmetric characteristic. The chlorosulfonic acid moiety and an amineof the diamine participate in a condensation reaction to yield asulfonamide-linked amine moiety and hydrochloric acid, and thus theaminating reagent may also include a base such as an aromaticunsymmetrical diamine to neutralize the evolved acid. The resultantsulfonamide-linked, amine-group-functionalized internal surface 110 mayserve as a weak base anion exchange material. Optionally, the process(process step 450 may expose the pendant amino moiety to a suitablemethylation reagent such as methyl iodide or dimethyl sulfate to producea pendant quaternary ammonium-group and thus a quaternaryamine-group-functionalized internal surface 110 serving as strong baseanion exchange material.

In some implementations, the sulfonamide-linked,amine-group-functionalized internal surface 110 of the column 100 iscoated with a layer of cation exchanging nanoparticles 132. In theseimplementations, electrostatic attraction between the positively chargedamine functional groups of the internal surface 110 and negativelycharged cation exchanging functional groups on the exterior surface ofCEX nanoparticles 132 electrostatically bonds the nanoparticles to theinternal surface 110, forming a monolayer that, like in the case of AEXnanoparticles on CEX surfaces, permits efficient stationary phase masstransfer to the CEX functional groups. For example, sulfonate- andcarboxylate-functionalized latex nanoparticles, such as thosemanufactured by Thermo Fisher Scientific (Waltham Mass.) for use in itsDionex IonPac CS10 (275 nanometer diameter cation exchange latexparticles with 5% crosslinking and sulfonic acid groups) and AcclaimTrinity Q1 (85 nanometer diameter cation exchange latex particles with2% crosslinking and carboxylic acid groups) cation exchange columns, tosuch functionalized internal surfaces. In process step 460 theamine-group-functionalized internal surface 110 of the capillary may beexposed to an aqueous suspension of cation exchanging nanoparticles 130.For example, a suspension of CS10 or Acclaim Trinity Q1 latexnanoparticles may be prepared by diluting a concentrated suspension with0.1 M hydrochloric acid in the case of the CS10 latex or using 0.1 Mammonium hydroxide in the case of Acclaim Trinity Q1 latex. Thesuspension may be pumped through the capillary using the system 300 ordual-system variant described above, or any other suitable pumpingapparatus. Finally, in process step 470 the coated internal surface 110of the capillary may be rinsed with deionized water to clean the coatedcolumn. For example, the column 100 may be connected to a HPLC pump andrinsed at 1 to 10 μL/min for 0.5 h to 2 h to remove the suspension fluidand unbound residual nanoparticles from the bore.

EXAMPLES AND RESULTS Working Example 1

-   -   Material: ZEONEX® 330R (norbornene-type cycloolefin polymer)    -   Dimensions: 370 μm o.d.; 28 μm i.d.    -   Sulfonation conditions: 2 h exposure to 95.1% ClSO₃H:4.9%        CH₃COOH @ 20-25° C.    -   Mean resultant cation exchange capacity: 3.2 peq./mm²

Working Example 2

-   -   Material: ZEONEX® 330R (norbornene-type cycloolefin polymer)    -   Dimensions: 370 28 μm o.d.; 28 μm i.d.    -   Sulfonation conditions: 6 h exposure to 95.1% ClSO₃H:4.9%        CH₃COOH @ 20-25° C.    -   Mean resultant cation exchange capacity: 70.1 peq./mm²

Working Example 3

-   -   Material: ZEONEX® 330R (norbornene-type cycloolefin polymer)    -   Dimensions: 370 μm o.d.; 28 μm i.d.    -   Sulfonation conditions: 2 h exposure to 95.1% ClSO₃H:4.9%        CH₃COOH, w/dissolved cycloolefin polymer reaction product, @        20-25° C.    -   Mean resultant cation exchange capacity: 23.9 peq./mm²

Working Example 4

-   -   Material: ZEONEX® 330R (norbornene-type cycloolefin polymer)    -   Dimensions: 370 μm o.d.; 28 μm i.d.;    -   Sulfonation conditions: 2 h exposure to 90% ClSO₃H:10% CH₃COOH @        20-25° C.    -   Mean resultant cation exchange capacity: 0.4 peq./mm²    -   Optional coating material: AS18 latex (65 nm particulate latex        with 8% crosslinking of alkanol quaternary ammonium)    -   Mean resultant anion exchange capacity: 17.8 peq./mm²

Working Example 5

-   -   Material: ZEONEX® 330R (norbornene-type cycloolefin polymer)    -   Dimensions: 370 μm o.d.; 28 μm i.d.;    -   Sulfonation conditions: 6 h exposure to 90% ClSO₃H:10% CH₃COOH @        20-25° C.    -   Mean resultant cation exchange capacity: 3 peq./mm²    -   Optional coating material: AS18 latex    -   Mean resultant anion exchange capacity: 28 peq./mm²        Sulfonation Process and Performance

To applicants' knowledge, there has not been any systematiccharacterization of the sulfonation of polyolefin materials, includingor excluding cycloolefin polymer materials, by chlorosulfonic acid. Ingeneral, sulfonation rate will be controlled by the concentration ofchlorosulfonic acid in the sulfonating reagent, the process temperature,and the exposure time of the material to the sulfonating reagent.Although it may be possible to use a sulfonating agent comprising purechlorosulfonic acid in an artificially cooled process, applicants havefound that at room temperature the pure acid attacks cycloolefin polymermaterials at an uncontrollable rate. For a process conducted at roomtemperature (20 to 25° C.), a sulfonating agent comprising 85 wt % to 95wt % chlorosulfonic acid has been found to produce a controllable andefficient reaction rate. FIG. 5 shows the degree of sulfonation observedversus time for a room temperature process 200 using a sulfonating agentcomprising 95.1 wt % ClSO₃H and 4.9 wt % CH₃COOH. The extent ofsulfonation was measured as picoequivalents (peq.) of cation exchangecapacity per unit surface area, assuming a nominal inner surface areaequal to that of a smooth, nonporous cylinder, for a norbornene-typecapillary material. The average extent of sulfonation with associatederror bars, for paired samples (two per time period), is shown for anotherwise identically processed set of 28 μm i.d. capillaries whereexposure to the sulfonating reagent was terminated at 2 h (WorkingExample 1; A), 4 h (B), 6 h (Working Example 2; C), 8 h (D), and 10 h(E), respectively. Between the first paired sample with 2 h exposure (A:3.2±2.7 peq/mm²) and the second paired sample with 4 h exposure (B:66.6±1.1 peq/mm²) the sulfonation extent increased dramatically, butonly modest further increases were seen in samples with 6 h (C) and 8 h(D) exposure. At 10 h exposure (E), sulfonation extent was significantlyless that that with 8 h exposure. As a benchmark, the theoreticallycomputed surface area occupied by a sulfonic acid group is 0.18-0.21 nm²(depending on its orientation [13]), from which one can compute amaximum monolayer coverage of 8 to 9 peq/mm² (note that the maximumcapacity of a thoroughly sulfonated macroporous 300 m²/g surface areacation exchange resin is ˜1 meq/g, translating to ˜3.3 peq/mm²).Therefore it is clear that for all but the 2 h exposure time, thesulfonation reaction must have continued well beyond a monolayercoverage. It is also important to note that the reported capacities wereobtained only after 100+ h of washing at high flow rates, at describedin step 240 and further discussed below. Without wishing to be bound bytheory, applicants believe that sulfonate group exchange capacitydramatically increases between 2 and 4 h of exposure due to reagentattack upon newly exposed underlayers of COP material, and that after 4h of exposure further sulfonation is accompanied by ring opening so asto produce dangling polymer chains that can be washed out of theinterior region 120, particularly off of the interior surface 110proper, over moderate periods of time. Even with pure water as theeluent, heavily sulfonated columns have been observed to exhibit greaterdetector noise that diminishes only with continued washing and someassociated loss of sulfonate functional group exchange capacity.

Applicants unexpectedly found that the sulfonation reaction isautocatalytic. When the sulfonating reagent contacts the COP material,some entity is formed that colors the sulfonating reagent, slowlytransforming it from clear to yellow to dark brown. This is accompaniedby an increase in sulfonating agent viscosity (flow rate through acapillary will decreases at constant pressure). FIG. 5 also shows thedegree of sulfonation observed versus time for a room temperatureprocess 200, using a ‘partially spent’ sulfonating reagent (95.1 wt %ClSO₃H and 4.9 wt % CH₃COOH after 24 h of contact with COP material,light yellow in color). This sulfonating reagent is much moreeffective—a paired sample with 2 h exposure (Working Example 3; F:23.9±1.1 peq/mm²) and a paired sample with 4 h exposure (G: 143.8±4.1peq/mm²) had significantly greater sulfonation extents thancorresponding pairs (A) and (B), respectively, with exposure to ‘fresh’sulfonating reagent. Preferably, to reduce required exposure time whilemaintaining reproducible sulfonation behavior, the sulfonating reagentis spiked with a chemical entity (or entities) produced by dissolving asmall amount of COP material in virgin sulfonation reagent over about 48h. For example, applicants' practice has been to place small sections ofCOP capillary (about 4 cm of collective length per gram of virginsulfonation reagent) in the sulfonation reagent about 48 h before use.It will be appreciated that other forms of COP material having a highsurface area to volume ratio could be used.

For the diluent, inert diluents like CHCl₃ or CH₂Cl₂ have beenrecommended for sulfonation reactions using ClSO₃H [12], but thesechlorinated solvents dissolve the COP substrate. Applicants have foundthat concentrated acids such as CH₃COOH, H₂SO₄, and CH₃SO₃H are suitablefor use as diluents. Other nonaqueous, chlorosulfonic acid compatiblematerials, including nitroaromatics such as nitrobenzene andnitroxylene, alkyl sulfonic acids such as ethane sulfonic acid andpropane sulfonic acid, and carboxylic acid anhydrides such as aceticanhydride, may also be used while maintaining compatibility withpolyolefin materials. Below about 80 wt % ClSO₃H, no sulfonation appearsto occur at room temperature in 24 h. Although sulfonation could beexpected to occur with ClSO₃H concentrations below 85-95 wt % atelevated process temperatures, COP capillaries cannot be heated beyondtheir comparatively limited glass transition temperature (e.g., 130 to150° C. for commercial COP materials). Beyond autocatalysis, sulfonationappears to be exclusively dependent on the ClSO₃Hconcentration—substituting H₂SO₄ for CH₃COOH does not produce anysignificant difference in sulfonation rate.

Depending upon exposure time, applicants have routinely attained columnswith a cation exchange (CEX) capacity of 200 peq/mm², and even exceeding300 peq/mm². For example, FIG. 6 shows a column capacity determinationfor an 870 mm long (effective length), 370 μm o.d./28 μm i.d. capillarysulfonated according to process steps 210-250 with exposure to a 95.1 wt% ClSO₃H and 4.9 wt % CH₃COOH sulfonating reagent, pumped bypressurizing reservoir 310 to 40 psi, for 5 h at room temperature.Column capacity was determined by regenerating the column with 5.4millimolar (mM) H₂SO₄, then monitoring for breakthrough of a 7.2 mM KOHsolution pumped at 0.21 μL/min. Observed capacity for the column was 305peq/mm². For comparative purposes, applicants have measured capacitiesof only ˜1 peq/mm² on PMMA columns (with native —COOH functional groups)after a strong base hydrolytic step [5].

Most cation exchange separations should be conducted with columns havinga sulfonate-group associated cation exchange capacity of at least 0.5peq/mm², up to about 4 peq/mm². However, highly sulfonated COP basedcolumns, much like highly sulfonated gel-type resins, show ion exclusionbehavior not previously reported for an open tubular capillary formatcolumn. FIG. 7 shows an exemplary chromatogram (a) for a highlyrepeatable separation of water and ethanol (50:50 ratio, 5 nL samplevolume) separated using a 750 mm long (effective length), 370 μm o.d./28μm i.d. capillary with a CEX capacity of 125±12 peq/mm² using a 0.5 mMHCl eluent pumped at 30 psi (flow rate of 200 nL/min). A clearseparation between the water and ethanol peaks is achieved. Theapplicants note that even when such highly sulfonated columns are coatedwith anion exchanging nanoparticles 130, the underlying sulfonatedregion 120 remains accessible, so that ion exchange and neutralretention behavior (through partition into the water phase associatedwith the sulfonate sites) proceeds simultaneously and can cause samplewater to be retained substantially more than some anionic analytes, asin exemplary chromatogram (b), or co-eluting with some strongly retainedanion, as in exemplary chromatogram (c). In the illustrated cases,separations were performed using an AS18 latex coated, 210 mm long(effective length) capillary with a CEX capacity of 1251±1 peq/mm² usinga 1.0 mM timesic acid (pH 4.5) eluent pumped at 13 psi (flow rate of 44nL/min). For chromatogram (b), the sample consisted of 1.5 nL ofsolution containing 0.5 mM chloride and sulfate. For chromatogram (c),the sample consisted of 1.5 nL of solution containing 0.5 mM chloride,sulfate, and perchlorate. Because perchlorate co-eluted with the waterpeak in this system, chromatogram (c) includes a plot showing the waterdip from a sample of deionized water for comparison. As mentioned above,the position of the water dip could be altered by altering the extent ofsulfonation of the column. Such mixed but independent retention modesmay offer intriguing possibilities for simultaneous separations ofanions from neutrals with appropriate detectors, as well as detection ofearly eluters that would otherwise be masked by the water dip.

Highly sulfonated columns (cation exchange capacity >200 peq/mm²)exhibit some decrease in exchange capacity upon prolonged washing withwater, with the effluent baseline conductance decreasing with increasingflow rate. This may indicate that conductive material is washing off theinterior surface 110 of the column 100, possibly oligomers or danglingopen chains from ring-opening sulfonation reactions. As shown in FIG. 8,both the baseline conductance and baseline noise reach a stable lowvalue only after extensive an extensive rinsing step of 20 to 100 h.

Coating Process and Performance

Packed columns including latex particles with extensively studiedselectivities have been developed, but have generally not been used insuppressed hydroxide open tubular capillary ion chromatography due tothe aforementioned instability of nanoparticle attachment to fusedsilica and PMMA materials. In going from —COOH based PMMA to —SO3Hfunctionalized COP, the present columns provide for a stronger,base-stable attachment to a fully ionized strong acid site. Withsufficiently large nanoparticles, e.g., AEX latex nanoparticles in therange of 60-200 nm, multilayer coverage by similarly charged materialsis unlikely, or at least has never been reported [14], which enablesconsistent mass transfer behavior of neutrals through thenanoparticulate layer to the sulfonate-functionalized region 120.Applicants have also experimentally observed performance consistent withmonolayer formation. Coating ˜1 peq/mm² CEX capacity PMMA columns withAS18 latex [5] produces AEX capacities of ˜10 peq/mm². Applicants'columns, coated according to process 200 and, specifically, steps250-260 as described above, can exhibit an increase in CEX capacity of650%, from 0.4 (Working Example 4) to 3 peq/mm² (Working Example 5) whenincreasing exposure time a 90% chlorosulfonic acid sulfonating reagentfrom 2 to 6 h; but, as shown in FIG. 9, upon coating with identicalsuspensions of AS18 latex nanoparticles, AEX capacity increases only by<60% from the least (Working Example 4, post-coating) to most sulfonated(Working Example 5, post-coating) examples. Indeed, for CEX capacitiesof 2-3 peq/mm² (>5 h sulfonation time in 90% chlorosulfonic acidsulfonating reagent), the AEX capacities were statisticallyindistinguishable (28.2±0.8 peq/mm²). Additionally, as shown in FIG. 10,for CEX capacities around ˜1 peq/mm² (open circles) AEX capacities of˜20 peq/mm² (open diamonds) are reproducibly realized with a coating of65 nm AS18 latex nanoparticles regardless of column i.d., suggestingthat much of the AEX capacity increase shown in FIG. 9 is due to theformation of an increasingly complete monolayer with increasinglycomplete sulfonation of the interior surface 110, not the formation of amultilayer coating of nanoparticles 130. Specifically, FIG. 10 showsresults for three pairs of columns (pairs 1-3: 370 μm o.d./28 μm i.d.capillary) and three single columns (columns 4-6: 370 μm o.d./19 μmi.d.) sulfonated by exposure 230 to a reagent comprising 87.8%ClSO₃:7.0% CH₃COOH:5.2% H₂SO₄ pumped at 15-50 psi for 4.5-5 hours (withthe exception of column 6, which was exposed to a reagent comprising87.7% ClSO₃:12.3% CH₃COOH under otherwise identical conditions), thenflushed as per step 230 and rinsed as per step 240 before exposure asper step 250 to an exemplary suspension of AS18 latex nanoparticles aspreviously described. Notably, in comparison to AS18 latex coated PMMAcolumns, the AEX capacity/unit area for the sulfonated COP basedcapillary columns is substantially greater. Electrostatically bondedlatex nanoparticles did not perceptibly wash off in 5 mM hydroxide,whereas in applicants' prior work such bonding was not stable under thesame conditions on PMMA. Specifically, columns coated with strong baseAEX materials including AS5A latex (a 60 nm particulate latex with 4%crosslinking and alkanol quaternary ammonium anion exchange sites), AS11latex (an 85 nm particulate latex with 6% crosslinking and alkanolquaternary ammonium anion exchange sites), AS16 latex (an 80 nmparticulate latex with 1% crosslinking and alkanol quaternary ammoniumanion exchange sites), AS18 latex (a 65 nm particulate latex with 8%crosslinking and alkanol quaternary ammonium anion exchange sites), andAminoPac PA10 (an 80 nm particulate latex with 20% crosslinking andalkyl ammonium anion exchange sites) maintained substantially the sameexchange capacity when exposed to 5 mM KOH eluents, and some (with AS5Aor AS18 latex coatings) would maintain substantially the same exchangecapacity when exposed to up to 50 mM KOH for periods of 40-48 hours. Itwill be appreciated that other AEX nanoparticles 130, including latexesand other substrates bearing weak base, AEX-functional aliphatic aminefunctional groups (e.g., AminoPac PA10 or Thermo Fisher ScientificA37353 latex beads, a 60 nm particulate latex with amine groups attachedto the terminus of aliphatic six-carbon spacer arms) could be employeddepending upon the intended column application.

Since high CEX capacities lead to increased noise and require prolongedwashing, an optimum combination of AEX capacity stability and baselinenoise will likely be obtained with intermediate CEX capacities andprolonged washing both before and after latex coating. Even with low CEXcapacity (1-3 peq/mm²), some columns showed excellent base stability,with AS5A latex coated columns showing no discernible loss of capacity(30.5±1.8 peq/mm²) over nearly 100 h of exposure to a 50 mM KOH eluent(interrupted only by intermittent capacity measurements). To put this inperspective in comparison with a commercial packed column, aconsideration of the applicable phase ratio is appropriate. In othertypes of chromatography the phase ratio is defined as the volume of themobile phase divided by the volume of the stationary phase; in an OTcapillary column the former is the volume of the bore [15]. In the caseof an ion exchange column, a more meaningful definition of the phaseratio β_(iex) with any specific eluent in the column would be the ratioof the number of ionic equivalents present in the mobile phase per unitlength of the column to the ion exchange capacity of the stationaryphase represented in the same length. Obviously, the higher this number,the less is the retention. For an AS5A column in the packed vs. 19 μm or28 μm bore OT format, Table 1 shows that the same eluent in an OT columnformat represents a 5-50× greater β_(iex), depending on the type oflatex used in the OT format coating 130; i.e., a proportionally lowereluent strength will be needed for an OT format column to obtain thesame retention factors.

TABLE 1 Phase Ratios of Commercial Packed Columns vs. OT Columns AminoPAC AS5A AS11 AS16 AS18 PA10 Packed Packed Packed Packed PackedCommercial Commercial Commercial Commercial Commercial Column ColumnColumn Column Column i.d., mm 4.0 4.0 4.0 4.0 2.0 L, mm 250 250 250 250250 Capacity, μeq 40 45 170 285 285 Cap., μeq/mm 0.16 0.18 0.68 1.141.14 Col. Vol/mm, mm³ 12.6 12.6 12.6 12.6 3.1 ¹Mob Phase Vol/mm, mm³ 5.05.0 5.0 5.0 1.3 ²Mob Phase IEX cap/mm, μeq 0.05 0.05 0.05 0.05 0.01β_(iex) 0.31 0.28 0.07 0.04 0.01 19 μm OTIC 19 μm OTIC 19 μm OTIC 19 μmOTIC 19 μm OTIC i.d., mm 0.019 0.019 0.019 0.019 0.019 Surface area,mm²/mm length 0.06 0.06 0.06 0.06 0.06 AEX Capacity, peq/mm² 30 25 11 34100 AEX Capacity, peq/mm length 1.79 1.49 0.66 2.03 5.97 Mob PhaseVol/mm, mm3 2.84E−04 2.84E−04 2.84E−04 2.84E−04 2.84E−04 ²Mob Phase IEXcap/mm, peq 2.84E+00 2.84E+00 2.84E+00 2.84E+00 2.84E+00 β_(iex) 1.581.90 4.32 1.40 0.48 28 μm OTIC 28 μm OTIC 28 μm OTIC 28 μm OTIC 28 μmOTIC i.d., mm 0.028 0.028 0.028 0.028 0.028 Surface area, mm²/mm length0.09 0.09 0.09 0.09 0.09 AEX Capacity, peq/mm² 30 30 30 30 100 AEXCapacity, peq/mm length 2.64 2.64 2.64 2.64 8.80 Mob Phase Vol/mm, mm36.16E−04 6.16E−04 6.16E−04 6.16E−04 6.16E−04 ²Mob Phase IEX cap/mm, peq6.16E+00 6.16E+00 6.16E+00 6.16E+00 6.16E+00 β_(iex) 2.33 2.33 2.33 2.330.70 Mob phase relative power 28 μm OTIC vs packed col 7.4 8.4 31.6 52.963.5 19 μm OTIC vs packed col 5.0 6.8 58.4 31.7 43.1 ¹Assumes a packingfraction of 60% ²Assumes 10 mM KOH eluentOverall Performance

Because the present columns have much greater capacity thancorresponding PMMA columns [16], higher eluent concentrations and/orshorter column lengths (requiring very low pressures) can be used. FIGS.11A and 11B illustrate operation with 22 cm (20 cm effective length) and32 cm (30 cm effective length) 370 μm o.d./19 μm i.d. columns,respectively, at applied pressures of 6.6 to 19 psi, attaining flowvelocities of 2.2-4.7 mm/s (flow rates of 39-80 nL/min), substantiallyabove the Van Deemter optimum (1.2 mm/s). As shown in FIG. 10A, thestandard 5 anion (F⁻ (peak 1), Cl⁻ (peak 2), NO₂ ⁻ (peak 3), Br⁻ (peak4), and NO₃ ⁻ (peak 5)) separation was possible within 4 min using 1.0mM Na-Benzoate (NaBz) as the eluent. The same ions can be baselineseparated in 1.6 min (the actual separation window being <45 s) with 5mM NaBz at 60 psi and in about 3 min at 30 psi. As shown in FIG. 11B,with a stronger eluent of 6.0 mM sodium salicylate (NaSal) and greatereffective length, a suite of seven anions including some very stronglyretained species (Cl⁻ (peak 2), ClO₃ ⁻ (peak 6), l⁻ (peak 7), SO₄ ²⁻(peak 8), SCN⁻ (peak 9), ClO₄ ⁻ (peak 10), and S₂O₃ ²⁻ (peak 11)) wereseparated within 3.5 min at 60 psi. Respectable plate numbers werepossible (best case efficiencies are as good as 93,000 and 128,000plates/m for fluoride and chloride, respectively, in FIG. 11A middle andFIG. 11B bottom). As shown in FIG. 12, a divalent ion-based eluent,e.g., a salt such as potassium hydrogen phthalate (KHP), can be used toseparate strongly retained anions and also offers the possibility ofmanipulating both eluent concentration and pH in order to change the ionelution orders, e.g., of SO₄ ²⁻ (peak 8) and ClO₃ ⁻ (peak 6) (2.0 mM KHPat pH 5.7 versus 10.0 mM KHP at pH 7.5), or S₂O₃ ²⁻ (peak 11) and l⁻(peak 7) (2.0 mM KHP at pH 5.7 versus 10.0 mM KHP at pH 5.7).

Coiled Open Tubular Format Capillary Columns

It is well-known that axial dispersion is the highest in a straighttube. Although the effects of deformed channels on mass transfer havebeen considered [17], and deformed connecting tubes have been used in atleast one commercial liquid chromatograph [18], verification andapplication at capillary scales has not been done, likely because thesilica capillaries in common use are brittle and exhibit a significantminimum bend radius. The present COP based capillaries have goodflexibility, especially at moderately elevated temperatures (e.g.,Zeonex® 330R has a glass transition temperature of 123° C., and a heatdistortion temperature of 103° C.). The disclosed capillaries can bereadily coiled with a bend radius, i.e., radius to the inside curvature,of at least about 0.8 mm (applicants have made helical coils with asmaller bend radius of 0.4 mm, but for these thick-walled capillariesthe inner surface appears to become damaged—using thin walledcapillaries and slowing the bending process would be likely to permitbend radii of at least 0.4 mm) up to about 2.0 mm where beneficialeffects become minimal. FIG. 13 shows exemplary COP based capillarycolumns that have been coiled with 0.4 mm and 0.8 mm bend radii(producing d_(c) values, equal to the inner diameter of the coil plusthe capillary tube diameter of 1.17 and 1.97 mm, respectively). FIG. 14shows an end view of the exemplary 0.8 mm bend radius column, with acorresponding inner diameter of the coil of about 1.6 mm, acorresponding outer diameter of the coil of about 2.3 mm, and a d_(c) of1.97 mm (the distance from bore to bore along a diameter of the column,or approximately the inner diameter plus the capillary diameter).

The column 100 may be coiled, when heated, around a form such as a rod.For example, applicants have heated straight capillaries in boilingwater and then wound the capillaries, while immersed, around 0.8 and 1.6mm diameter metal rods. The formed, helically coiled column may then beallowed to cool and removed from the form. Preferably, the ends 302 and304 of the capillary are kept straight and taped off to prevent waterfrom entering the capillary during coiling (if water or another heatedfluid is used; it will be appreciated that air or other gasses couldalso be used in automated coiling processes). Such ends 302 and 304would also permit coiling prior to performance of the process 200,although, as discussed below, coiling can also be performed aftersulfonation and coating.

Qualitatively, the centrifugal component in helical flow (the pressureis slightly greater than for a straight tube of identical length)flattens the parabolic velocity profile across the bore, reducing axialdispersion while simultaneously increasing mass transport to the wall.The key parameter is the Dean number N_(De)=N_(Re)*√{square root over(d_(t)/d_(c)))} where N_(Re) is the Reynold's number, d_(t) and d_(c)are the bore diameter and coil diameter, respectively; with centrifugaleffects increasing with increasing N_(De) (essentially zero for straighttubes or large diameter coils). FIG. 15 shows Van Deemter curves for achloride analyte run on an 733 mm long (effective length), 370 μmo.d./19 μm i.d. AS18 latex coated COP based open tubular capillarycolumn using a 4.0 mM sodium salicylate (NaSal) eluent pumped at variousflow velocities (from 0.05 to 0.9 cm/s). The same column was firstemployed as a straight separation column (782 mm total length), thenformed into a d_(c)=1.97 mm column like that that shown in FIGS. 13-14and employed as a helically coiled separation column (with 674 mm ofcolumn length being coiled). Coiling perceptibly improves the columnefficiency for chloride, and the same effect is observed for theunretained water dip. Experimentally, the minimum plate height forchloride changes from 5.9 to 5.7 μm; with the absolute differences inplate heights increasing with increasing flow velocity. The respectivebest fits to the Van Deemter Equation (i.e., h=B/u+C*u) for the straightand coiled columns are:

straight column h = 1.91 × 10⁻⁵/u + 2.66 × 10⁻³ s⁻¹*u coiled column h =1.83 × 10⁻⁵/u + 2.46 × 10⁻³ s⁻¹*uwhere h is in cm and u is in cm/s. The B-term and, especially, theC-term both decrease on coiling.

The pressure drop along the column 100 is greater when formed intohelical coil versus a straight configuration. The difference betweenconfigurations will be proportional to the ¼th power to the square rootof N_(De), depending upon the specific conditions [15]. In oneexperiment, the pressure drop of a 78.2 cm long, 19 μm i.d. straightcolumn was measured at different flow rates, and then the samemeasurements were repeated as the column was partially coiled for 22.5cm, 45.5 cm, and 67.5 cm of the column length around a 0.8 mm diametersupport rod. FIG. 16 shows that the overall increase in pressure uponcoiling to 0.4 mm bend radius can be given by the equation:additional ΔP/u (psi·s/cm)=(3.4±0.1)×10⁻²*cm of tubecoiled+0.12±0.28  Eq. (1)and that the pressure drop increase for coiling to this comparativelysmall diameter helical coil is equivalent to a ˜24% increase in straightcolumn length.

CONCLUSION

In summary, the applicants have disclosed sulfonated polyolefin basedopen tubular capillary separation columns, and AEX nanoparticle coated(sulfonated polyolefin based) open tubular capillary anion separationcolumns, which can survive hydroxide eluents of high enoughconcentrations to carry out charge-based separations, and thus makingthem uniquely suitable for Suppressed Conductometric Open Tubular IonChromatography (SC-OTIC) as otherwise described in U.S. patentapplication Ser. No. 15/258,493, the entirety of which is incorporatedby reference. The AEX capacities of exemplary coated COP OT columns canbe 2× or more of those of AEX coated PMMA and silica columns. Platecounts for 19 μm i.d. columns can exceed 125,000 plates/m, so that withan effective length of only 20-30 cm, the same as that of traditionalpacked columns, the disclosed columns can provide good separation ofmany common anions in a short period with appropriate eluents. Theflexibility of the polyolefin materials allows the capillaries to becoiled with sub-mm bend radii, resulting in a significant increase incolumn efficiency. Some polyolefin materials, such as a commerciallyavailable norbornene-based COP material, advantageously offer reasonablytransparent windows at for optical spectrometry that add to the columns'versatility.

REFERENCES

-   [1] Cheong, W. J.; Ali, F.; Kim, Y. S.; Lee, J. W. J. Chromatogr. A    2013, 1308, 1-24.-   [2] Pyo, D. J.; Dasgupta, P. K.; Yengoyan, L. S. Anal. Sci. 1997, 13    (suppl), 185-190.-   [3] Breadmore, M. C.; Macka, M.; Avdalovic, N.; Haddad, P. R.    Analyst 2000, 125, 1235-1241.-   [4] Zhang, S. S.; Macka, M.; Haddad, P. R. Electrophoresis 2006, 27,    1069-1077.-   [5] Zhang, M.; Yang, B. C.; Dasgupta, P. K. Anal. Chem. 2013, 85,    7994-8000.-   [6] Yang, B. C.; Zhang, M.; Kanyanee, T.; Stamos, B. N.;    Dasgupta, P. K. Anal. Chem. 2014, 86, 11,554-11,561.-   [7] http://www.cyclo-olefin-polymers.com/Whats the difference    between COP and COC.aspx-   [8] (sono, T.; Satoh, T. in Encyclopedia of Polymeric Nanomaterials,    Kobayashi, S.; Műllen, K. Eds, Springer, 2014. pp 1-8.-   [9] Zeon Co.    http://www.zeon.co.jp/business_e/enterprise/speplast/speplast1_8.html-   [10] Knox, J. H.; Gilbert, M. T. J. Chromatogr. 1979, 186, 405-418.-   [11] Bakker, B. H.; Cerfontain, H. Eur. J. Org. Chem. 1999 (1),    91-96.-   [12] Cremlyn, R. J. W. Chiorosulfonic Acid: A Versatile Reagent;    Royal Society of Chemistry: Cambridge, UK, 2002.-   [13]    http://www.chemicalize.org/structure/#!mol=sulfonic+acid+ion&source=fp-   [14] Slingsby, R. W.; Pohl, C. A. J. Chromatogr. 1988, 458, 241-253.-   [15] International Union of Pure and Applied Chemistry (IUPAC). “The    Gold Book”. http://goldbook.iupac.org/P04531.html-   [16] Zhang, M.; Stamos, B. N.; Dasgupta, P. K. Anal. Chem. 2014, 86,    11,547-11,553.-   [17] Halasz, I. Journal of Chromatography 1979, 173, 229-247.-   [18] Perkin-Elmer Corp. The TriDet HPLC, see e.g.,    http://pubs.acs.org/doi/pdf/10.1021/ac00281a734.-   [19] Ramshankar, R.; Sreenivasan, K. R. Phys. Fluids 1988, 31,    1339-1347.

What is claimed is:
 1. An open tubular capillary column for liquid andion chromatography, the column comprising: an ionically impermeablecapillary of a polyolefin material; the capillary having a bore with aninternal surface that has been exposed to a sulfonating reagentcomprising chlorosulfonic acid (ClSO₃H) to sulfonate the polyolefinmaterial to a sulfonated polyolefin material, wherein, after exposure tothe sulfonating reagent, the internal surface has been exposed to anasymmetrical diamine aminating agent to form a sulfonamide-linked,amine-group-functionalized internal surface.
 2. The open tubularcapillary column of claim 1, wherein the aminating reagent comprisedN—N-dimethylethylenediamine.
 3. The open tubular capillary column ofclaim 1, wherein, after exposure to the aminating agent, the internalsurface has been exposed to a methylating agent to form asulfonamide-linked, quaternary-amine-group-functionalized internalsurface.
 4. The open tubular capillary column of claim 1, wherein thebore further includes a coating formed by exposing thesulfonamide-linked, amine-group-functionalized internal surface to asolution of suspended cation exchanging nanoparticles.
 5. The opentubular capillary column of claim 4, wherein the suspended cationexchanging nanoparticles are sulfonate-group- orcarboxylate-group-functionalized latex nanoparticles.
 6. A process formanufacturing an open tubular capillary column for liquid and ionchromatography, the process comprising: exposing an internal surface ofa capillary tube manufactured from a polyolefin material to asulfonating reagent including chlorosulfonic acid to sulfonate thepolyolefin material.
 7. The process of claim 6, wherein the sulfonatingagent comprises from 85 wt % to 95 wt % chlorosulfonic acid, and theinternal surface is exposed to the sulfonating agent for at most 8hours.
 8. The process of claim 6, further comprising exposing thesulfonated internal surface of the capillary tube to a nonaqueous,chlorosulfonic acid compatible flushing agent.
 9. The process of claim8, further comprising rinsing the flushed and sulfonated internalsurface of the capillary tube with deionized water.
 10. The process ofclaim 8, further comprising: after exposure to the flushing agent,exposing the sulfonated internal surface of the capillary tube to asuspension of anion exchanging nanoparticles to electrostatically bondthe anion exchanging nanoparticles to the sulfonated internal surface.11. The process of claim 8, further comprising: after exposure to theflushing agent, exposing the sulfonated internal surface of thecapillary tube to an asymmetrical diamine aminating agent to form asulfonamide-linked, amine-group-functionalized internal surface.
 12. Theprocess of claim 11, wherein the asymmetrical diamine aminating agentcomprises N—N-dimethylethylenediamine.
 13. The process of claim 12,further comprising: after exposure to the aminating agent, exposing theinternal surface of the capillary tube to a methylating agent to form asulfonamide-linked, quaternary-amine-group-functionalized internalsurface.
 14. The process of claim 13, wherein the methylating agent ismethyl iodide or dimethyl sulfate.
 15. The process of claim 13, furthercomprising: after exposure to the aminating agent, exposing the internalsurface of the capillary tube to a suspension of cation exchangingnanoparticles to electrostatically bond the cation exchangingnanoparticles to the amine-group-functionalized internal surface.
 16. Anopen tubular capillary column for liquid and ion chromatography, thecolumn comprising: an ionically impermeable polyolefin capillary; thecapillary having a bore with a sulfonamide-linked,amine-group-functionalized internal surface.
 17. The open tubularcapillary column of claim 16, wherein the amine-group-functionalizedinternal surface provides a quaternary amine group.
 18. The open tubularcapillary column of claim 16, wherein the bore further includes acoating of cation exchanging nanoparticles electrostatically bound tothe amine-group-functionalized internal surface.
 19. The open tubularcapillary column of claim 18, wherein the cation exchangingnanoparticles are comprised of sulfonate-group- orcarboxylate-group-functionalized latex nanoparticles.
 20. The opentubular capillary column of claim 18, wherein the cation exchangingnanoparticles form a monolayer over the sulfonamide-linked,amine-group-functionalized internal surface.
 21. The open tubularcapillary column of claim 16, wherein capillary has asulfonate-group-functionalized region disposed under the internalsurface of the bore.
 22. The open tubular capillary column of claim 16,wherein the polyolefin material comprises a cycloolefin polymer.
 23. Theopen tubular capillary column of claim 22, wherein the polyolefinmaterial comprises a norbornene-type polymer.